CN1166576C - Scale and/or corrosion inhibiting composition - Google Patents

Scale and/or corrosion inhibiting composition Download PDF

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Publication number
CN1166576C
CN1166576C CNB008032459A CN00803245A CN1166576C CN 1166576 C CN1166576 C CN 1166576C CN B008032459 A CNB008032459 A CN B008032459A CN 00803245 A CN00803245 A CN 00803245A CN 1166576 C CN1166576 C CN 1166576C
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composition
acid
aspartic acid
poly aspartic
oligopolymer
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CN1339015A (en
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���ֶ�����÷��
帕沃尔·克梅克
��E����Ĭ��ϣ
德怀特·E·埃默里希
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Suo Li Cisco Skill Cayman Co
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Ashland Inc
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F5/00Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents
    • C02F5/08Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents
    • C02F5/10Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents using organic substances
    • C02F5/14Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents using organic substances containing phosphorus
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23FNON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
    • C23F11/00Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
    • C23F11/08Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids
    • C23F11/10Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids using organic inhibitors
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23FNON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
    • C23F11/00Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
    • C23F11/08Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids
    • C23F11/10Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids using organic inhibitors
    • C23F11/173Macromolecular compounds
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23FNON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
    • C23F14/00Inhibiting incrustation in apparatus for heating liquids for physical or chemical purposes
    • C23F14/02Inhibiting incrustation in apparatus for heating liquids for physical or chemical purposes by chemical means
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/08Corrosion inhibition

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Metallurgy (AREA)
  • Mechanical Engineering (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Water Supply & Treatment (AREA)
  • Environmental & Geological Engineering (AREA)
  • Hydrology & Water Resources (AREA)
  • Preventing Corrosion Or Incrustation Of Metals (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Physical Vapour Deposition (AREA)
  • Agricultural Chemicals And Associated Chemicals (AREA)
  • Flanged Joints, Insulating Joints, And Other Joints (AREA)
  • Lift Valve (AREA)
  • Glass Compositions (AREA)
  • Protection Of Pipes Against Damage, Friction, And Corrosion (AREA)
  • Coloring Foods And Improving Nutritive Qualities (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
  • Medicines Containing Plant Substances (AREA)
  • Detergent Compositions (AREA)
  • Paints Or Removers (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)
  • Curing Cements, Concrete, And Artificial Stone (AREA)
  • Processing Of Solid Wastes (AREA)
  • Adhesives Or Adhesive Processes (AREA)

Abstract

This invention relates to scale and/or corrosion inhibiting compositions for aqueous systems comprising (a) polyaspartic acid, and (b) a water soluble phosphonated oligomer. The compositions are effective scale inhibitors and corrosion inhibitors, but are also advantageous from an environmental standpoint because they are non-toxic, contain no heavy metals, and have little phosphorus. They also have significant calcium/hardness tolerance and are chlorine/bromine stable.

Description

Suppress fouling and/or corrosion compositions
Technical field
The present invention relates to a kind of inhibition fouling and/or corrosion compositions that is used for aqueous systems, it comprises: (a) poly aspartic acid and (b) water-soluble phosphoric acid salinization oligopolymer.Said composition is effective scale inhibitor and corrosion inhibitor, and sees it also is favourable from the viewpoint of environment, because they are atoxic, do not contain heavy metal and contains a spot of phosphorus.They also have tangible calcium/hardness tolerance and are that chlorine/bromine is stable.
Background technology
The water that is used in industry cooling or mining system is taken from rivers, lake, pond or groundwater reservoir.This kind water comprises the dissolved inorganic salt.When these water in cooling system by heat exchanger and cooling tower circulation time since vaporization losses a part of water.This has increased the concentration of inorganic salt in system.If surpass the solubleness of these salt in water, will precipitate.
Be deposited in along with salt on the internal surface of cooling system, they form fouling or settling.Fouling has suppressed effective heat to be shifted, and has limited flowing of water, and has promoted to form the corrosion under the settled layer.As a result, must remove fouling by cleaning.This cleaning is expensive, because necessary closing device produces labour cost, and delayed production.Consider these problems, prevent from that incrustation scale from forming preferably to remove fouling.
Fouling can be under an embargo to water treatment system by adding chelating or complex compound.Required chelating/complex compound is based on the stoichiometry of calcium and magnesium cation content in the aqueous systems that is cleaned.This method that suppresses fouling is expensive and does not use usually.
Before more than 50 year, find that some compound is as extremely effective scale inhibitor.This kind compound is to use and be referred to as " threshold values inhibitor " with the significantly lower amount of stoichiometry.The example of threshold values inhibitor is phosphonate and water-soluble acrylic/toxilic acid/sulfonic acid polymer or multipolymer.Corrosion inhibitor for example phosphonate, inorganic phosphate, pyrroles, zinc and molybdate often is to use with scale inhibitor.
Except effective usefulness, Water Treatment Chemicals must be acceptable on the environment.Environmental legislation bans use of the corrosion inhibitor that resembles chromic salt and so on, and general limitation is used all heavy metals now.Other trend is, Water Treatment Chemicals is atoxic, has a small amount of or do not have phosphorus, has high calcium/hardness tolerance, and stable to chlorine/bromine, and has high fouling and corrosion efficient simultaneously.Because these requirements, the Cost Growth of water causes higher utilization again/higher refrigeration cycle, and this has caused the water coolant of high hardness and alkaline matter content.
US5,523,023 relate to a kind of poly aspartic acid and tricarboxylic composition of phosphinylidyne butane of comprising, and it is as alkaline cleaner.US5,386,038 disclose the phosphatization oligopolymer with following general formula:
H[CHRCHR] n-PO 3M 2
Wherein, at least one R base is COOM in each unit, CH 2OH, sulfonic group or phosphono, and another R base can be identical or different with first R group, is hydrogen or COOM, hydroxyl, phosphono, sulfonic group, sulfate, C 1-7Alkyl, C 1-7Alkenyl or carboxylicesters, the C that phosphono, sulfonic group, sulfate and/or hydroxyl replace 1-7Alkyl or C 1-7Alkenyl, and each M be positively charged ion so that the phosphatization oligopolymer is water miscible, and n is 1-6.These compositions have suppressed fouling and/or have been exposed to the corrosion of metal of aqueous systems.
Summary of the invention
The present invention relates to a kind of be used to suppress aqueous systems for example water coolant, the water and have high rigidity and the fouling and/or the corrosion compositions of the GEOTHERMAL WATER of alkalescence of digging up mine, its water-soluble phosphoric acid salinization oligopolymer that comprises significant quantity (a) poly aspartic acid and (b) have a following general formula forms to suppress fouling:
H[CHRCHR] n-PO 3M 2
Wherein, at least one R base is COOM in each unit, CH 2OH, sulfonic group or phosphono, and another R base can be identical or different with first R group, is hydrogen or COOM, hydroxyl, phosphono, sulfonic group, sulfate, C 1-7Alkyl, C 1-7Alkenyl or carboxylicesters, the C that phosphono, sulfonic group, sulfate and/or hydroxyl replace 1-7Alkyl or C 1-7Alkenyl, and each M be positively charged ion so that the phosphatization oligopolymer is water miscible, and n is 1-6, usually greater than 1 with less than 6.
Composition is a synergistic action effect, because they are than the fouling of expecting of inhibition to a greater degree with regard to the fouling inhibition of single component is active.Said composition is qualified on the environment, because they are atoxic, does not contain heavy metal, and contains and contain phosphorus on a small quantity or not.They have tangible calcium/hardness tolerance, and are stable to chlorine/bromine, and have suppressed corrosion effectively.
Embodiment
The component of scale inhibitor composition (a) is the water-soluble poly aspartic acid.For the purposes of this invention, term " poly aspartic acid " should be intended to comprise the salt and the derivative of poly aspartic acid.The derivative of poly aspartic acid and salt thereof and poly aspartic acid be know and at US5, introduction is arranged in 523,023, it is hereby incorporated by.The preferred use is that the molecular weight of gel osmoticing chromatogram analysis method is 500-10000, preferably 1000-5000, the most preferably poly aspartic acid of 2000-4000.Poly aspartic acid preferably with the form of salt, particularly uses with the form of sodium salt or sylvite.Whether poly aspartic acid uses the pH that depends on handled aqueous systems with the form of acid or salt.The salt of poly aspartic acid is sodium salt preferably.The derivative that also can use poly aspartic acid is the acid anhydrides of poly aspartic acid for example, its under working conditions because hydrolysis can be transformed into poly aspartic acid.
The component of scale inhibitor composition (b) is a water-soluble phosphine carboxylic acyl oligopolymer salt, and particular certain cancers finds it is the mixture of oligopolymer usually.These oligopolymer are to be described in US5, and in 386,038, its content is drawn at this and is reference.The general structure of these water-soluble phosphine carboxylic acyl oligopolymer is:
H[CHRCHR] n-PO 3M 2
Wherein, at least one R base is COOM in each unit, CH 2OH, sulfonic group or phosphono, and another R base can be identical or different with first R group, is hydrogen or COOM, hydroxyl, phosphono, sulfonic group, sulfate, C 1-7The alkane alkyl, C 1-7Alkenyl or carboxylicesters, phosphono, sulfonic group, sulfate, and/or the C of hydroxyl replacement 1-7Alkane alkyl or C 1-7Alkenyl, and each M be positively charged ion so that the phosphatization oligopolymer is water miscible, and n is 1-6, usually greater than 1 with less than 6.
The preferred water-soluble phosphine carboxylic acyl oligopolymer salt that uses is the following specific class salt with said structure general formula:
H[CH (CO 2Na)-CH (CO 2Na)] nPO 3Na 2Wherein n is 1 to 5.
The weight ratio of phosphatization oligopolymer and poly aspartic acid is 8: 1 to 1: 12, preferred 4: 1 to 1: 9, and more preferably 1: 4 to 1: 9.
For some application; the preferred water solubility copolymer that adds is to the fouling composite inhibiting; phosphono-carboxylic acids polymkeric substance for example; toxilic acid or maleic anhydride polymkeric substance; acrylate copolymer; the multipolymer of methacrylate polymer and they and sulfonic acid functional group and/or phosphono functional group, preferably vinylformic acid/sulfonic acid copolymer or vinylformic acid/maleic acid.
Other selectable component comprises the phosphinylidyne butane tricarboxylic acid, tolyl-triazole, orthophosphoric acid salt, polyphosphate, hydroxy ethylene diphosphonic acid, amino three (methylene phosphonic acids).
The fouling composite inhibiting has suppressed the formation of lime carbonate, calcium phosphate, calcium sulfate and other scale forming matter.They particularly are used within the pH value scope of 8.0-9.0 and temperature is 40-65 ℃.The fouling composite inhibiting is to use with the minimum dose of 0.1ppm, but 5.0-500.0ppm preferably most preferably is 10.0-200.0ppm.
Shortenings
Following is the shortenings of using in an embodiment:
AA:AAMPS ACUMER 2000 vinylformic acid/sulfonic acid copolymer are by Rohm ﹠amp; Haas Co
Produce.
Vinylformic acid/sulfonic acid copolymer that AR-540 is produced by Alco Chemical Inc.
BTC phosphinylidyne butane tricarboxylic acid is also referred to as the Am into Bayhibit, by Bayer Co.
Produce.
MPY corrosion rate unit: millimeter/year.
The PAA poly aspartic acid is referred to as VPOC 2401, is produced by Bayer Co..
The water mixture of PCM phosphono-carboxylic acids oligopolymer salt is referred to as BRICORR
288, by Albright ﹠amp; Wilson Inc produces
The following example will illustrate specific embodiments of the present invention.They are not considered to limit application of the present invention.It should be noted that other embodiment also is utilizable.
Embodiment 1 (inhibition of calcium carbonate scaling threshold values)
With standard lime carbonate wobbler test the fouling inhibition of the blend of several inhibition foulings of containing PCM and PAA is assessed.Several contrasts have also been assessed.
Step comprises: add scale inhibitor composition sample (by the consumption shown in Table I and the II) to a solution that places 125 milliliters of wobbler flasks, this solution comprises 90.0 milliliters of DI water, 5.0 milliliters of calcium strong solution (14.7 gram CaCl 2.2H 2The O/ liter) and 5.0 milliliters of alkaline strong solutions ((1.59 gram Na 2CO 3+ 14.8 gram NaHCO 3)/liter).The water parameter of the initial testing of gained is: as CaCO 3Calcium=500ppm, as CaCO 3Total alkalescence=500ppm and PH=8.5).Then flask is covered and it was placed 16-18 hour in 50 ℃ on wobbler.After the time of shaking, whole sample solution is passed through Whatman #5 filter paper filtering.With filtrate then with the titration of 0.01MEDTA solution to determine to be retained in the content of the calcium in the test soln.The result is shown in Table I and the Table II, wherein each suppress per-cent be the mean value of 5 revision tests and wherein the inhibiting per-cent of calcium be by following calculating:
% threshold values restraining effect (%TI)=[(ppm A-ppmB) ÷ (500-ppmB)] * 100
Wherein:
The initial calcium concn of 500=500ppm lime carbonate
After the ppm A=test, in filtrate as CaCO 3The calcium concn of ppm; With
After the ppm B=test, in blank solution as CaCO 3The calcium concn of ppm.
The %TI of Table I PCM/PAA blend
PCM ppm solid content PAA ppm solid content PCM: PAA ratio %TI
25.0 0.0 25∶0 54.1±7.5
20.0 5.0 4∶1 56.4±6.5
12.5 12.5 1∶1 56.8±4.9
5.0 20.0 1∶4 60.0±6.0
3.1 21.9 1∶7 70.6±3.1
2.5 22.5 1∶9 57.4±4.0
0.0 25.0 0∶25 12.0±1.7
Result in table 1 has shown the threshold values restraining effect per-cent of PCM/PAA blend.For 4: 1 to 1: 9 solids ratios, the PCM/PAA blend of 1: 4 to 1: 9 ppm solids ratio particularly, synergetic property is to show significantly.
Table II shows result and the additional test result of selecting from Table I.Set test result to determine whether the PCM/PAA multipolymer shows synergetic property.
The synergistic effect of Table II blend
Has only PCM Has only PAA 1: 7 32.1 70.6+38.5 2.5+22.5 of 1: 4 51.9 60.0+8.1 3.1+21.9 of the difference amplification ppm+ppm %TI %TI %TI 5+20 of the reality of PCM/PAA blend PCM+PAA ratio prediction 1: 9 20.4 57.4+37.0
ppm %TI ppm %TI
5.0 39.0 20.0 12.9
3.1 21.0 21.9 11.1
2.5 8.5 22.5 11.9
Data in the Table II show that PCM and PAA multipolymer reach the obvious higher %TI value (actual value) than theoretical prediction.Difference between actual value and the predictor is 8.1% to 38.5%.
Embodiment 2 rotors are bathed the corrosion test method
Soft steel (C1010) sample tube is tested as corrosion inhibitor with described composition.Use " rotor bath corrosion test " evaluation group compound.Step comprises: add in the corrosion inhibitor composition (consumption shown in the Table III) the surveyed a kind of solution to the sample cylinder, this solution comprises 7.8 liters of softening waters, 100.0 milliliters of rigid strong solutions (every liter 70.6 gram CaCl 2.2H 2O adds 42.0 gram MgCl 2.6H 2O), and 100.0 milliliters of strong solutions (whenever be upgraded to 8.5 gram Na 2CO 3+ 20.2 gram NaHCO 3+ 35.5 gram Na 2SO 4).The pH value of water is adjusted to 8.5.The soft steel sample tube is suspended from the water in the test jar by mandrel, and mandrel is attached on the driving gear again.Heating also makes water temperature remain on 50 ℃.Driving gear is opened with its standard speed.After 4 all day, close system, remove sample tube, clean and calculate the erosion rate of representing with MPY.With the results are shown in the Table III of the mean value of twice revision test.The result of this corrosion test is shown in down in the Table III.
The Table III rotor is bathed the result of corrosion test
PCM, the ppm solid content PAA, the ppm solid content MPY
25.0 0.0 20.1
20.0 5.0 9.8
15.0 10.0 6.5
10.0 15.0 6.1
5.0 20.0 10.8
0.0 25.0 NA 1
When independent use, known PAA is extremely weak and is insufficient corrosion inhibitor.This test-results has confirmed this point.This test-results shows that also PCM is weak and is insufficient corrosion inhibitor.Yet, show that the blend of PCM and PAA has much lower corrosion rate, confirmed that PCM and PAA suppress the corrosive synergetic property.
1Annotate: the corrosion inhibition rate of the PAA that uses is not to be presented in the Table II separately, because thick scale deposition is arranged on sample tube and therefore to compare with all the other tests (the not sample tube of fouling) to be invalid.

Claims (12)

1, suppress fouling and/or corrosion compositions, it comprises: (a) poly aspartic acid and (b) have the water-soluble phosphate oligopolymer salt of following general formula:
H[CHRCHR] n-PO 3M 2
Wherein, at least one R base is COOM in each unit, CH 2OH, sulfonic group or phosphono, and another R base can be identical or different with first R group, is hydrogen or COOM, hydroxyl, phosphono, sulfonic group, sulfate, C 1-7Alkyl, C 1-7Alkenyl or carboxylicesters, the C that phosphono, sulfonic group, sulfate and/or hydroxyl replace 1-7Alkyl or C 1-7Alkenyl, and each M be positively charged ion so that the phosphatization oligopolymer is water miscible, and n is 1-6, and
(b) it is 4: 1 to 1: 9 with (a) weight ratio.
2, composition as claimed in claim 1, n is greater than 1 and less than 6 in the wherein said general formula.
3, composition as claimed in claim 1, wherein water-soluble phosphoric acid salinization oligopolymer has following general formula:
H[CH(CO 2Na)-CH(CO 2Na)] nPO 3Na 2
Wherein n is 1 to 5.
4, composition as claimed in claim 1, wherein poly aspartic acid is to be selected from poly aspartic acid, its salt, its derivative and their mixture.
5, composition as claimed in claim 1, wherein the molecular-weight average of poly aspartic acid is 500 to 10000 by gel permeation chromatography.
6, composition as claimed in claim 5, it comprises at least a annexing ingredient, this annexing ingredient is selected from vinylformic acid/sulfonic acid copolymer, vinylformic acid/maleic acid and their mixture.
7, composition as claimed in claim 6, wherein the weight ratio of phosphatization oligopolymer and poly aspartic acid is 1: 4 to 1: 9.
8, composition as claimed in claim 7, wherein the molecular-weight average of poly aspartic acid is 2000 to 4000 by gel permeation chromatography.
9, composition as claimed in claim 8, it comprises at least a annexing ingredient, this annexing ingredient is selected from tolyl-triazole, benzotriazole, orthophosphoric acid salt and polyphosphate.
10, a kind of each described composition that uses claim 1-9 suppresses the method for fouling in aqueous systems, it is characterized in that, described composition is added in the described aqueous systems, and wherein said composition is to use with the concentration of 5ppm to 200ppm.
11, method as claimed in claim 10, wherein said fouling is a lime carbonate.
12, a kind of each described composition of claim 1-9 that uses suppresses corroding method in aqueous systems, it is characterized in that, described composition is added in the described aqueous systems, and wherein said composition is to use with the concentration of 5ppm to 200ppm.
CNB008032459A 1999-01-28 2000-01-26 Scale and/or corrosion inhibiting composition Expired - Lifetime CN1166576C (en)

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US09/238,850 1999-01-28
US09/238,850 US6207079B1 (en) 1999-01-28 1999-01-28 Scale and/or corrosion inhibiting composition

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CN1166576C true CN1166576C (en) 2004-09-15

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